Surface clogging process modeling of suspended solids during urban stormwater aquifer recharge

Aquifer recharge,which uses urban stormwater,is an effective technique to control the negative effects of groundwater overexploitation,while clogging problems in infiltration systems remain the key restricting factor in broadening its practice.Quantitative understanding of the clogging process is still very poor.A laboratory study was conducted to understand surface physical clogging processes,with the primary aim of developing a model for predicting suspended solid clogging processes before aquifer recharge projects start.The experiments investigated the clogging characteristics of different suspended solid sizes in recharge water by using a series of one-dimensional fine quartz sand columns.The results showed that the smaller the suspended particles in recharge water,the farther the distance of movement and the larger the scope of clogging in porous media.Clogging extents in fine sand were 1 cm,for suspended particle size ranging from 0.075 to 0.0385 mm,and 2 cm,for particles less than 0.0385 mm.In addition,clogging development occurred more rapidly for smaller suspended solid particles.It took 48,42,and 36 hr respectively,for large-,medium-,and small-sized particles to reach pre-determined clogging standards.An empirical formula and iteration model for the surface clogging evolution process were derived.The verification results obtained from stormwater recharge into fine sand demonstrated that the model could reflect the real laws of the surface clogging process.     

多种染料的微生物脱色研究

从印染、毛纺等废水处理场的生物膜和活性污泥中分离到13株对36种染料有脱色能力的细菌。其中三株转化单胞菌D_(32),D_(33),D_4分别对29种染料有良好的脱色作用,其完整细胞对单一染料的脱色活力达2.6mg·g~(-1)(细胞湿重)·h~(-1)。对脱色反应的条件和机理进行了初探。     

Behaviors and kinetics of toluene adsorption‐desorption on activated carbons with varying pore structure

This work was undertaken to investigate the behaviors and kinetics of toluene adsorption and desorption on activated carbons with varying pore structure. Five kinds of activated carbon from different raw materials were selected. Adsorption isotherms and breakthrough curves for toluene were measured. Langmuir and Freundlich equations were fitted to the equilibrium data, and the Freundlich equation was more suitable for simulating toluene adsorption. The process consisted of monolayer, multilayer and partial active site adsorption types. The effect of the pore structure of the activated carbons on toluene adsorption capacity was investigated. The quasi-first-order model was more suitable for describing the process than the quasi-second-order model. The adsorption data was also modeled by the internal particle diffusion model and it was found that the adsorption process could be divided into three stages. In the external surface adsorption process, the rate depended on the specific surface area. During the particle diffusion stage, pore structure and volume were the main factors affecting adsorption rate. In the final equilibrium stage, the rate was determined by the ratio of meso-and macro-pores to total pore volume. The rate over the whole adsorption process was dominated by the toluene concentration. The desorption behavior of toluene on activated carbons was investigated,and the process was divided into heat and mass transfer parts corresponding to emission and diffusion mechanisms, respectively. Physical adsorption played the main role during the adsorption process.     

南京冬季市区和郊区气溶胶中PAHs浓度的昼夜特征及粒径分布

为了研究南京市区与郊区气溶胶中多环芳烃(PAHs)污染状况和分布特征,利用气-质联用仪(GC-MS)分析了2010年1月1～10日日间和夜间分别在南京大学和南京信息工程大学采集的气溶胶样品,得到南京市区与郊区17种PAHs浓度,总浓度分别为41.36～220.35 ng.m-3和45.10～200.86 ng.m-3,其中约66%～67%分布于细粒子(Dp≤2.1μm)中.研究发现,南京市区和郊区气溶胶中PAH总浓度均处于较高的水平;但两者昼夜变化趋势不同,即市区PAH总浓度日间高于夜间,郊区PAH总浓度日间低于夜间.主导风向的改变和高压天气系统对PAH浓度变化影响较大;在市区其影响主要表现在细粒子部分,而郊区主要表现在粗粒子部分.市区和郊区不同环数的PAHs粒径分布不同;2～3环PAHs,郊区含量高于市区;而4～6环PAHs,市区含量高于郊区.高环数(4～6环)PAHs在粗模态出现较大浓度峰可能是由于南京地区粗模态气溶胶中碳含量较高.市区和郊区相似的特征比值说明两者的PAHs具有相同污染来源,主要为生物质及煤的燃烧和汽车尾气,表明南京市区PAHs受到郊区工业源排放影响较大.     

漆酶对活性黑KN-B和直接大红染料的脱色性能

利用白腐真菌漆酶对活性黑KN-B和直接大红2种偶氮染料进行脱色实验。考察反应时间、加酶量、pH值、染料浓度、温度对脱色率的影响,研究了ABTS介体以及金属离子存在下的脱色效果,并分析了漆酶脱色的动力学性能以及其对偶氮染料的降解规律。结果表明,活性黑KN-B和直接大红脱色适宜条件为：反应时间为30 min,加酶量8 U/mL,pH=7,染料浓度分别为50 mg/L和80 mg/L,温度40~45℃。ABTS介体对酶促偶氮染料脱色没有明显促进作用。Fe²⁺对漆酶脱色有较强的抑制作用;Cu²⁺对漆酶催化活性黑KN-B促进作用较大,对直接大红影响较小。漆酶对2种染料的脱色反应符合米氏方程,其催化活性黑KN-B和直接大红染料的K_m值分别为114.81 mg/L,317.5 mg/L,v_max值分别为6.57 mg/（L·min）和26.0 mg/（L·min）。     

基于稳定氢同位素的太原市大气单环芳烃来源

采集太原市城北和城南区域环境空气和5类污染源挥发性有机物样品,测定样品中典型单环芳烃稳定氢同位素（δD）组成,基于同位素质量平衡原理计算单环芳烃从源到环境空气受体的δD初始混合值,探讨单环芳烃来源.结果表明,柴油挥发源、溶剂挥发源、汽油挥发源（97^#）、汽油挥发源（95^#）、机动车尾气（97^#）、机动车尾气（95^#）和民用燃煤源中单环芳烃δD范围依次为：（-138.7‰~-115.5‰）、（-147.0‰~-121.0‰）、（-150.8‰~-117.6‰）、（-131.8‰~-113.8‰）、（-171.2‰~-120.0‰）、（-138.9‰~-102.7‰）和（-168.3‰~-142.3‰）,民用燃煤源中单环芳烃δD显著贫重氢同位素（D）组成,机动车尾气源与汽油挥发源中苯的δD相比显著贫D,可用于探索污染物转化过程;城北和城南环境空气中δD范围为（-131.7‰~-115.1‰）和（-131.9‰~-74.9‰）,δD初始混合值为-138.4‰和-173.9‰,体现了其来源差异.     

邻苯二甲酸二丁酯的微生物降解

通过驯化富集培养,从处理石化厂废水的活性污泥中分离出１株邻苯二甲酸酯降解菌ＦＳＩ,研究了邻苯二甲酸酯菌ＦＳＩ对邻苯二甲酸二丁酯的生物降解特性。邻苯二甲酸酯降解菌ＦＳＩ降解最适酸度为ｐＨ６．５～８．０,温度为２０～３５℃。菌株ＦＳＩ对邻苯二甲酸二丁酯的生物降解反应速率遵循一级反应动力学模式。试验结果表明,菌株ＦＳＩ对邻苯二甲本二丁酯具有高效降解作用。     

三段A/O工艺处理发制品产业集聚区综合废水

利用三段A/O工艺作为发制品产业集聚区综合废水生物处理单元,探讨了不同进水流量分配比和污泥回流比下COD、TN、PO₄^3--P的去除性能和微生物群落特征.结果表明,在进水流量分配比60%：25%：15%、污泥回流比75%、缺氧区与好氧区容积比1：1、SRT 20d、HRT 16h条件下,三段A/O工艺处理综合废水后出水TN平均浓度14.85mg/L,COD浓度低于40m/L;此时PO₄^3--P去除率达到最大值,为56.21%.参与处理综合废水的主要门水平微生物Proteobacteria和Bacteroidetes的相对丰度是45.63%~60.13%和16.65%~30.55%.Denitratisoma、Thauera、uncultured-f-Saprospiraceae和Sulfuritalea等优势菌属相对丰度的增加,是三段A/O工艺TN去除率随第一分段进水流量分配比增大或污泥回流比降低而提高的本质体现.     

一株降解邻苯二甲酸酯真菌的筛选及其降解特性研究

采用富集培养法,从PAEs污染的农田土壤中筛选出1株邻苯二甲酸酯类化合物(PAEs)降解真菌F9,经形态学特征及18S rDNA序列分析,初步鉴定为爪哇正青霉(Eupenicillum javanicun).通过正交试验研究,得出菌株F9的最优降解条件是:C:N为20:1、pH为7.0、最佳PAEs初始浓度为50 mg·L^-1.菌株F9对土壤中复合PAEs(DMP、DEP和DOP)有良好的降解效果.在30 d培养期内,可将灭菌土壤中300 mg·kg^-1的PAEs降解65.2%,且培养第一阶段(0~15 d)的降解率远高于第二阶段(16~30 d).     

采用高效菌提高普通活性污泥系统抗2,4-DCP负荷冲击能力

研究了用于处理生活污水的普通活性污泥反应器(CAS)受到2,4-二氯酚(2,4-DCP)间歇性负荷冲击时,投加高效菌的生物强化系统和对照系统对污染物的响应及系统稳定性,并考察了长期运行过程中强化系统对目标污染物去除能力的变化.结果表明,投加5%和15% 2,4-DCP复合高效菌的强化CAS系统,其对目标污染物的降解能力及抗负荷冲击能力得到显著提高.当系统受到间歇性2,4-DCP负荷冲击[110.37～171.60 mg/(L·d)]时,对于单次投菌后前30日内发生的间歇性负荷冲击,强化系统有效保持了对目标污染物的强化效果;在无2,4-DCP存在的情况下连续运行70d,当系统再次受到2,4-DCP负荷冲击时,强化系统的强化效果与前几次相比已明显下降,不能够快速有效去除污染物并维持系统稳定,因此有必要再次投加高效菌.